Process for the preparation of copolymers

- Shell Oil Company

A process for the preparation of a copolymer of carbon monoxide with an olefinically unsaturated compound in which a powder of a copolymer of carbon monoxide with an olefinically unsaturated compound is suspended in a liquid diluent. The suspension is contacted with a catalyst composition which is soluble in the diluent and which is based on a Group VIII metal and a bidentate ligand. The catalyst composition is used in such a quantity that in the polymerization mixture more than 0.1 mmoles of the Group VIII metal is present per liter of liquid phase.

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Claims

1. A process for the preparation of a copolymer of carbon monoxide with an olefinically unsaturated compound, which process comprises suspending a powder of a copolymer of carbon monoxide with an olefinically unsaturated compound in a liquid diluent in which the copolymer to be prepared forms a suspension and subsequently contacting the monomers in the suspension so obtained with a catalyst composition which comprises a Group VIII metal and a bidentate ligand of the formula R.sup.5 R.sup.6 M.sup.1 --R--M.sup.2 R.sup.7 R.sup.8, wherein M.sup.1 and M.sup.2 independently represent a phosphorus, nitrogen, arsenic or antimony atom, R.sup.5, R.sup.6, R.sup.7 and R.sup.8 independently represent an optionally polar substituted hydrocarbyl group, at least one of R.sup.5, R.sup.6, R.sup.7 and R.sup.8 represents a polar substituted hydrocarbyl group, and R represents a bivalent organic bridging group containing at least one carbon atom in the bridge, wherein said catalyst composition is used in such a quantity that in the polymerization mixture greater than 0.1 mmoles of the Group VIII metal is present (calculated per liter of liquid phase).

2. A process as claimed in claim 1, wherein the Group VIII metal is present in the polymerization mixture in a quantity of at least 0.15 mmoles (calculated per liter of liquid phase).

3. A process as claimed in claim 1 wherein the catalyst composition contains palladium as the Group VIII metal, M.sup.1 and M.sup.2 represent phosphorus atoms, one or more of R.sup.5, R.sup.6, R.sup.7 and R.sup.8 represents an aryl group and R represents a bivalent organic bridging group containing from 2 to 4 bridging atoms, at least two of which are carbon atoms.

4. A process as claimed in claim 3 further comprising, as an additional catalyst component, a source of anions selected from the group consisting of protic acids, tetrahydrocarbylborate anions and carborate anions, Lewis acids and alumninoxanes, which anions are applied in a quantity of from 0.5 to 25 equivalents per gram atom of Group VIII metal.

5. A process as claimed in claim 3, further comprising, as an additional catalyst component aluminoxanes applied in such a quantity that the molar ratio of aluininum to the Group VIII metal is in the range of from 2000:1 to 100:1.

6. A process as claimed in claim 1 wherein the copolymer of carbon monoxide with an olefinically unsaturated compound is suspended in a quantity of 0.1-20% w, relative to the weight of the liquid phase.

7. A process as claimed in claim 1 wherein the copolymer of carbon monoxide with an olefinically unsaturated compound suspended in the liquid diluent is based on the same monomers as the copolymer to be prepared.

8. A process as claimed in claim 1 wherein the bulk density of the suspended copolymer is in the range of 50-1000 kg/m.sup.3.

9. A process as claimed in claim 1 wherein the olefinically unsaturated compound is selected from the group consisting of ethene, propene, butene-1 and mixtures thereof.

10. A process as claimed in claim 1 carried in a protic diluent, at a temperature in the range of from 30 to 150.degree. C. and a pressure in the range of from 1 to 10 MPa, with the molar ratio of carbon monoxide to olefinically unsaturated compound(s) selected in the range of 1:2 to 2:1, and using a quantity of catalyst composition in the range of 10.sup.-6 to 10.sup.-2, calculated as moles of Group VIII metal per mole of olefinically unsaturated compound to be copolymerized with carbon monoxide.

11. A process for the preparation of a copolymer of carbon monoxide with an olefinically unsaturated compound, which process comprises copolymerizing the monomers in the presence of a copolymer obtained in a process as claimed in claim 1 as a supported catalyst.

Referenced Cited
U.S. Patent Documents
5658982 August 19, 1997 Baardman et al.
5668249 September 16, 1997 Baardman et al.
5670611 September 23, 1997 Baardman et al.
Foreign Patent Documents
340844 November 1989 EPX
453011 A2 October 1991 EPX
614928 A2 September 1994 EPX
619334 A1 October 1994 EPX
733660 September 1996 EPX
Other references
  • Search Report dated Feb. 17, 1998.
Patent History
Patent number: 5905138
Type: Grant
Filed: Feb 19, 1997
Date of Patent: May 18, 1999
Assignee: Shell Oil Company (Houston, TX)
Inventor: Johannes Adrianus Maria Van Broekhoven (CM Amsterdam)
Primary Examiner: Samuel A. Acquah
Attorney: Todd F. Volyn
Application Number: 8/801,977